Reaction-rectification-separation-refinement novel method, technique and device of ethylene glycol and 1,2-butanediol

A separation method and technology of a reactive distillation column are applied in the field of processes and devices, separation methods of ethylene glycol and 1,2-butanediol, and can solve the problems of affecting the yield of ethylene glycol, unfavorable energy saving, poor recovery and the like , to achieve the effect of high quality recycled products, saving equipment investment, and low relative volatility

Active Publication Date: 2016-05-04
TIANJIN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] 1. Patent CN101928201 discloses a purification process for the crude product of coal-based ethylene glycol. The purification process is obtained from the crude product of coal-based ethylene glycol through saponification reaction, methanol removal, hydrogenation reaction, three-tower rectification and adsorption treatment. High-purity ethylene glycol products, but 1,2-butanediol is only removed by azeotropy with ethylene glycol, which not only causes the loss of 1,2-butanediol, a high value-added product, but also affects the Yield of diol
[0006] 2. Patent CN102276418 proposes to use a mixture of ethylene glycol and 1,2-butanediol from the process of oxalate hydrogenation to ethylene glycol products, by using at least one of ZSM-5, Y-type zeolite or beta zeolite An adsorbent that absorbs 1,2-butanediol to obtain the purification of ethylene glycol. However, the recovery rate of ethylene glycol is not indicated, and the recovery and utilization of 1,2-butanediol is not involved.
[0007] 3. Patent CN103193594 discloses a method for separating and purifying ethylene glycol from the liquid phase product of oxalate hydrogenation by using a dioxane compound immiscible with ethylene glycol as an entrainer and using azeotropic distillation method, the liquid phase mixture passes through two light removal towers to remove low-boiling compounds such as methanol and methyl glycolate, and then enters the azeotropic rectific

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  • Reaction-rectification-separation-refinement novel method, technique and device of ethylene glycol and 1,2-butanediol
  • Reaction-rectification-separation-refinement novel method, technique and device of ethylene glycol and 1,2-butanediol
  • Reaction-rectification-separation-refinement novel method, technique and device of ethylene glycol and 1,2-butanediol

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Embodiment 1

[0066] The method of the present invention is used for ethylene glycol and 1,2-butanediol mixture reactive distillation separation process, such as figure 1 As shown, including acetal reactive distillation column (T11), aldehyde recovery column (T12), acetal product separation column (T13), acetal product hydrolysis distillation column (T21, T31), ethylene glycol purification column (T22 ), 1,2-butanediol purification column (T32), condenser, reboiler, pump and related feed lines and lines connecting the above equipment. The diol mixed raw material S01 (the molar ratio of ethylene glycol and 1,2-butanediol: 0.6:0.4) enters the reactive distillation column (T11) with 21 theoretical plates from the sixth theoretical plate, and the reactant acetaldehyde is removed from the column. The kettle enters the reactive rectification tower, the total amount of reactants and the molar ratio of diol are 1.19:1, and the reaction section is set below the diol feed position to the tower kettle...

Embodiment 2

[0069] The method of the present invention is used for ethylene glycol and 1,2-butanediol mixture reactive distillation separation process, such as figure 2 As shown, it is the improvement process of embodiment 1, and the acetal reactive rectifying tower (T11) and the acetaldehyde recovery tower (T12) in the original process are merged into the acetal reactive rectifying tower (T112), including the acetal reactive rectifying tower (T112). Distillation column (T112), acetal product separation column (T13), acetal product hydrolysis and rectification column (T21, T31), ethylene glycol purification column (T22), 1,2-butanediol purification column (T32), Condenser, reboiler, pump and associated feed lines and lines connecting the above equipment. The diol mixed raw material S01 (the molar ratio of ethylene glycol and 1,2-butanediol: 0.6:0.4) enters the reactive distillation column (T112) with 30 theoretical plates from the 15th theoretical plate, and the reactant acetaldehyde is ...

Embodiment 3

[0072] The method of the present invention is used for ethylene glycol and 1,2-butanediol mixture reactive distillation separation process, such as figure 2 As shown, for the improved process of Example 1, it is considered to separate the acetal product of 1,2-butanediol as a product without hydrolysis, including the acetal reactive distillation column (T11) and the aldehyde recovery column (T12) , acetal product separation tower (T13), ethylene glycol acetal product hydrolysis and rectification tower (T21), ethylene glycol purification tower (T22), 1,2-butanediol acetal product purification tower (T41), Phaser (D1), condenser, reboiler, pump and associated feed lines and lines connecting the above equipment. The other operations of the third embodiment are the same as those of the first embodiment. The extracted stream S20 of the acetal product separation tower (T13) is cooled to 65°C and then enters the phase separator D1, phase-separated at 1 atm and 65°C, the water phase...

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Abstract

The invention relates to a separation method, technique and device of ethylene glycol and 1,2-butanediol. The method comprises the following steps: reacting a diol mixture and aldehyde or ketone in a reaction rectification tower by acetal or ketal reversible reaction to generate an acetal/ketone mixture, rectifying to separate the acetal/ketone mixture, and carrying out reaction, rectification and hydrolysis to obtain the high-purity ethylene glycol and 1,2-butanediol products. By using the technique for separation and purification, the purity of the main product ethylene glycol can reach 99.9% or above, the recovery rate can reach 99.5% or above, and the purity of the 1,2-butanediol product can reach 98.5% or above. By using the reaction rectification method, the difficulty in separating azeotropic ethylene glycol and 1,2-butanediol with approximate variable boiling point and low relative volatility becomes the problem of separation of the separable acetal/ketone product, thereby effectively implementing the high-efficiency separation on the ethylene glycol and 1,2-butanediol.

Description

technical field [0001] The invention belongs to the field of chemical distillation and separation, and relates to a separation method, process and device of ethylene glycol and 1,2-butanediol. Background technique [0002] As an important basic organic chemical raw material, ethylene glycol is mainly used in the production of polyester fibers, antifreeze, unsaturated polyester resins, lubricants, plasticizers, nonionic surfactants and explosives. Alcohols can also be used in coatings, photographic developers, brake fluids and inks, etc., as solvents and media for ammonium perborate, and in the production of special solvents such as glycol ethers, which are widely used. And some studies have pointed out that ethylene glycol has great development potential in the field of liquid fuel cells in the future. my country is a big consumer of ethylene glycol, and the domestic output of ethylene glycol is far from meeting its own needs. In 2014, my country's ethylene glycol output wa...

Claims

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Application Information

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IPC IPC(8): C07C29/74C07C29/88C07C31/20
CPCC07C29/74C07C29/88C07C31/202C07C31/207Y02P20/10
Inventor 高鑫李鑫钢李洪黄伟进丛山
Owner TIANJIN UNIV
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